Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
  • B01F27/05—Stirrers
  • B01F27/11—Stirrers characterised by the configuration of the stirrers
  • B01F27/113—Propeller-shaped stirrers for producing an axial flow, e.g. shaped like a ship or aircraft propeller
  • B01F27/1132—Propeller-shaped stirrers for producing an axial flow, e.g. shaped like a ship or aircraft propeller with guiding tubes or tubular segments fixed to and surrounding the tips of the propeller blades, e.g. for supplementary mixing
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
  • B01F27/05—Stirrers
  • B01F27/11—Stirrers characterised by the configuration of the stirrers
  • B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
  • B01F27/1123—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades sickle-shaped, i.e. curved in at least one direction
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
  • B01F27/05—Stirrers
  • B01F27/11—Stirrers characterised by the configuration of the stirrers
  • B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
  • B01F27/1125—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
  • B01F27/25—Mixers with both stirrer and drive unit submerged in the material being mixed

Definitions

• the present invention relates to mixers arranged to be submersed into a liquid and operable for stirring the liquid by means of a propeller which is driven in rotation.
• the invention also relates to a method for controlling the flow through a mixer assembly.
• the mixers referred to are used mainly to generate and maintain a motion within a volume of liquid, in order to prevent sedimentation or agglomeration of solid matter that is dispersed in the liquid, or for de-stratification of liquids having different densities, for homogenization or for the mixing of substances in liquid, etc.
• Typical implementations include waste water treatment, water purification, PH- neutralization, chlorine treatment processes, cooling applications, de-icing applications, manure treatment processes, e.g.
• the typical mixer comprises a propeller that is driven by an electric motor.
• the motor is contained in a motor enclosure which protects the motor and electrical components from the surrounding liquid.
• a motor shaft extends from an end of the motor enclosure to mount the propeller's hub in axial relation to the motor and motor enclosure.
• the opposite end of the motor enclosure may be arranged with mountings by which the mixer can be supported from a wall of a liquid-holding container, albeit other mountings are also conceivable.
• the propeller usually has at least two propeller vanes supported from a propeller hub to reach radially with respect to a propeller axis.
• a singular propeller vane could be arranged to run helically about a propeller hub.
• the propeller causes a drop in pressure on a suction side thereof, and a corresponding raise in pressure on the pressure side.
• the pressure difference results in a liquid flow through the propeller, from the suction side to the pressure side thereof. Since the pressure side is typically facing from the motor and motor enclosure, the main flow is usually directed axially away from the mixer.
• the propeller thus generates in rotation an axial thrust, the size of which is determined by the design of the hydraulic components of the mixer, propeller design, rotational speed, and motor capacity.
• the stirring result which is related to the capacity of the mixer to generate a circulating flow in a bulk of liquid is largely depending on the efficiency of the mixer to create a jet flow downstream of the propeller.
• the significance of an extended jet flow is readily appreciated in connection with the stirring of waste water containing solid matter such as fibrous material and heavy organic particles that consume the energy introduced by the mixer.
• the volume/ time flow through the propeller is high resulting in a mainly axial flow.
• the propeller however also generates a rotational motion in the liquid.
• the total energy is increased in terms of static pressure and kinetic energy.
• the static pressure provides the axial thrust
• the kinetic energy which is usually not advantageous in the subject mixer applications, is the result of a rotational component of motion induced in the liquid as it passes the propeller. In order to achieve maximum static pressure/ axial thrust, it would thus be desired to suppress the rotation of the liquid that exits from the mixer's propeller.
• Propeller vane design in general is a well documented art. It is known (by the Equation of Momentum) that axial thrust is proportional to the increase in axial velocity through the mixer. The magnitude and direction of the flow generated by propeller blades and vanes can be demonstrated by applying velocity triangles to a section of the propeller, as taught by e.g. Stepanoff (1948, reprint 1993): “Centrifugal and Axial Flow Pumps” (Chap. 3. 1 and 3.5).
• the propeller section considered here for the analysis is a stream surface defined by the rotation RD around the axis A of the "streamline" SL showed in Fig. 1.
• the streamline SL starts upstream the propeller, passes the propeller blade leading edge LE and ends downstream the trailing edge TE.
• Fig Ia shows velocity triangles for a stream surface example, diagrammatically illustrated.
• the absolute velocities C at the leading and trailing edges of the propeller section may be determined for a number of stream surfaces.
• the flow and absolute velocity vector is void of any circumferential component and is therefore parallel to the propeller axis.
• a mixer with a ring-shaped envelope about the propeller, known as a jet ring.
• the purpose and operation of the jet ring is to ensure that liquid is drawn mainly axially into the propeller on the suction side.
• the ring is typically supported by struts reaching towards the propeller from the motor enclosure.
• the ring and struts are however not contemplated and effective for control or neutralization of a rotational motion in the flow that exits the propeller.
• baffles are optionally used when prevention of a non-axial flow from the tube is occasionally asked for.
• Still another problem related with the prior art mixers is torsional stress and vibration resulting from the reactive forces acting on the mixer and its supporting structures.
• an object of the present invention is to provide enhanced axial thrust and extended jet flow from the propeller of a mixer which is submersed in liquid during operation.
• an object of the present invention is to provide enhanced axial thrust and extended jet flow from the propeller of a mixer which during operation is submersed in liquid containing fibrous material and solid matter.
• an object of the present invention is to provide a mixer wherein flow control means are designed to avoid clogging and obstruction from solids included in the liquid.
• an object of the present invention is to provide a mixer avoiding the formation of vortexes that allow air to reach the propeller on the suction side.
• an object of the present invention is to provide a mixer which provides reduced torsional stress and vibration.
• a mixer assembly comprises a motor; a motor shaft; a propeller connected to the motor shaft and in operation driven by the motor in a first direction of rotation about a propeller axis, the propeller fully submersed in liquid during operation and in rotation generating liquid flow from a suction side to a pressure side of the propeller.
• the mixer assembly is characterized in that flow control vanes are arranged on the suction side of the propeller, and oriented in an axial plane to deflect the liquid from axial flow into a flow containing a circumferential component of direction which is opposed to the direction of rotation of the propeller.
• the flow control vanes are curved when viewed in the axial plane.
• the flow control vanes may additionally have a compound curvature, thus being curved also in a radial plane perpendicular to the propeller axis.
• the flow control vanes are designed with a stream surface which generates in the liquid flow, for each streamline through the propeller, a circumferential velocity component that fully neutralizes a circumferential velocity component generated by a corresponding stream surface of the propeller blade, resulting in an essentially axial exit flow from the propeller.
• the propeller is connected to a motor shaft extending from a motor which is encased in a liquid-tight motor casing and submersed in the liquid during operation.
• the pressure side of the propeller blade faces away from the motor casing, and the flow control vanes are supported from the motor enclosure to reach with slanting leading edges towards the suction side of the propeller.
• the leading edge of the flow control vane may be designed to have a slanting orientation, far from being orthogonal to the flow direction. This embodiment is advantageous in that clogging caused by solids and fibrous matter comprised in the liquid can be effectively prohibited.
• This embodiment not only provides a compact design, but provides also effective flow control on the suction side of the propeller and further reduces propagation of vortex forming rotation in the liquid on the suction side of the propeller.
• the number of flow control vanes can be adapted to a subject mixer, preferably at least four to six flow control vanes are arranged and equidistantly spaced about the propeller axis.
• a ring-shaped envelope /jet ring may be supported concentrically about the propeller from one or several of the free ends of the flow control vanes.
• the angular orientation of the flow control vanes may be adjustable in relation to the propeller axis.
• the method further comprises the step of forming the flow control vanes with stream surfaces that, for each streamline through the propeller, are adapted to a corresponding stream surface of the propeller blade.
• Fig. 1 is an elevation view showing a mixer
• Fig. Ia illustrates diagrammatically velocity triangles of a liquid flow through a stand alone propeller in a mixer of prior art
• Fig. 2 is an end view of the mixer of fig. 1 ;
• Fig. 3 is a perspective view of the mixer of figs. 1 and 2;
• Fig. 4 is an elevation view showing a mixer assembly according to the present invention.
• Fig. 4a illustrates diagrammatically velocity triangles of a liquid flow through a vane and propeller assembly in a mixer according to the present invention
• Fig. 5 is an end view of the mixer assembly of fig. 4;
• Figs. 5a and 5b illustrate schematically the orientation and shape of flow control vanes included in the mixer assembly
• Fig. 6 is a perspective view of the mixer assembly of figs. 4 and 5;
• Fig. 7 is an elevation view showing a further development of the mixer assembly of figs. 4-6;
• Fig. 8 is an end view of the mixer assembly of fig. 7, and
• Fig. 9 is a perspective view of the mixer assembly of figs. 7 and 8. Detailed description of a preferred embodiment of the Invention
• a mixer comprising a motor 1 shown in broken lines in fig. 1 , a motor shaft 2 likewise shown in broken lines in fig. 1 , and a propeller 3 connected to the motor shaft 2 and in operation driven in rotation by the motor 1.
• the propeller 3 comprises propeller blades 4 which are supported from a propeller hub 5, the hub 5 in turn connectable to the motor shaft 2.
• the propeller comprises two vanes 4, each of which comprises a pressure side P and a suction side S (see fig. 1).
• the direction of rotation is illustrated by the arrow RD in the end view of fig.
• the propeller in rotation about a propeller axis A effecting a liquid flow in a direction as is generally illustrated by the arrow FD in fig. 1. More precisely, and illustrated in fig. 3, the propeller in rotation imparts to the liquid also a circumferential component of direction, resulting in a non-axial flow as indicated by the arrow RF in fig. 3.
• the motor 1 is enclosed in a liquid-tight casing 6, to which power may be supplied via cables that are omitted from the drawings.
• Means for supporting the mixer in a fully submerged position in liquid are typically arranged on the casing 6.
• attachment means may be arranged on the casing for suspending the mixer from structures that reach into the liquid from above, or from the bottom or from a wall of a container containing the volume of liquid that is to be treated by the mixer in operation.
• the mixer shown in figs. 1 -3 is to be seen merely as one example of mixers to which the present invention can be implemented. Other designs are thus conceivable, as long as they provide a propeller which in operation is fully submerged into the liquid, and a motor arranged for rotation of the propeller via a motor shaft.
• a mixer assembly 10 according to the present invention is illustrated.
• the mixer assembly 10 is shown in connection with the mixer of figs. 1 -3, albeit as explained above the casing, the motor and propeller components may be otherwise designed.
• the mixer assembly 10 thus incorporates a motor, a motor shaft and a propeller, in operation generating a flow of liquid from the suction side of the propeller to the pressure side thereof.
• flow control vanes 1 1 are arranged on the suction side S of the propeller.
• the flow control vanes 1 1 are oriented to effect deflection of the liquid from a substantially axial flow on the suction side S into a flow which upon entry into the propeller blade contains a circumferential component of direction which is opposed to the direction of rotation RD of the propeller blade.
• the orientation of the flow control vanes 1 1 is such, that when a sectional profile SP of a flow control vane 1 1 is orthogonally projected onto an axial plane AP through the propeller axis, that sectional profile SP has an angular orientation relative to the propeller axis A.
• the control vanes 1 1 may have an essentially straight sectional profile SP as illustrated in fig. 5a, or a curved sectional profile SP as illustrated in fig. 5b.
• the flow control vanes 1 1 may have a compound curvature, including a curved sectional profile also in a radial plane perpendicular to the propeller axis A.
• Fig. 4a shows diagrammatically the result achievable through the introduction of flow control vanes 1 1 on the suctions side S of the propeller.
• the flow control vanes 1 1 are supported from the motor casing 6 to extend at a slanting orientation towards the propeller. Connected to the motor casing in the base ends, the control vanes reach with their free ends
• the flow control vanes 1 1 will typically be equidistantly distributed about the propeller axis A, at a number of at least four and preferably at least six or more flow control vanes.
• the flow control vanes 1 1 are preferably shaped to have a slanting and optionally convex leading edge 13 facing opposite the flow direction of liquid into the propeller, at an angle ⁇ substantially larger than 90°.
• the slanting configuration further improves the ability to prevent solids and fibrous matter from attaching to the flow control vanes 1 1.
• the flow control vanes advantageously terminate with a trailing edge 13' positioned close to the propeller on the suction side S.
• the connection of the base end of the flow control vane may comprise a mechanism for adjusting the angular orientation of the flow control vanes relative to the propeller axis A.
• the adjustment mechanism may include pivotal connections 14 between the base end and the motor casing 6, as well as pivotal connections 15 between the base end and a ring member 16 which is rotatably journalled in the motor casing.
• the efficiency of the mixer assembly 10 is further improved through the application of a ring-shaped envelope 17 concentrically about the mixer's propeller.
• the envelope or jet ring 17 comprises a straight cylinder section 18 facing towards the pressure side P, and an outwardly flared cylinder section 19 adjoining the cylinder section 18 on the suction side S.
• the jet ring 17 is supported in one or several of the free ends 12 of the control vanes 1 1 , the free ends connecting to the flared cylinder section 19 of the jet ring.
• Still another advantageous effect is achieved from applying flow control on the suction side of a submerged mixer propeller in liquid mixing applications as taught herein.
• the flow control vanes 1 1 effectively counteract the propagation of rotational flow from the propeller to the liquid volume on the suction side of the propeller, which is frequently observed in prior art mixer applications. This way, vortex formation on the suction side is also considerably reduced or avoided through the teachings provided herein.
• the advantages provided by controlling the liquid flow on the suction side of the mixer propeller as taught herein can be achieved in modified embodiments of the mixer assembly.
• One modification includes, e.g., a bevel gear transmission submerged together with the mixer propeller and driven by a motor which is supported above the liquid.
• the flow control vanes can be supported on the bevel gear transmission.
• the flow control vanes can be supported from a motor shaft encasing separated from the motor encasing, e.g. Still another embodiment foresees that the flow control vanes are supported from a separate structure positioned on the suction side of the propeller, such as a structure attached to the liquid container.
• a separate structure positioned on the suction side of the propeller, such as a structure attached to the liquid container.

Landscapes

• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Engineering & Computer Science (AREA)
• Aviation & Aerospace Engineering (AREA)
• Mixers Of The Rotary Stirring Type (AREA)

Priority Applications (6)

Applications Claiming Priority (2)

Publications (1)

Family

ID=40853299

Family Applications (1)

Country Status (9)

Cited By (2)

Families Citing this family (5)

Citations (2)

Family Cites Families (22)

• 2008
  • 2008-01-11 SE SE0800071A patent/SE531903C2/sv unknown
• 2009
  • 2009-01-12 PL PL09701040.9T patent/PL2227315T3/pl unknown
  • 2009-01-12 US US12/811,431 patent/US8764278B2/en not_active Expired - Fee Related
  • 2009-01-12 WO PCT/SE2009/050012 patent/WO2009088356A1/en active Application Filing
  • 2009-01-12 ES ES09701040.9T patent/ES2581935T3/es active Active
  • 2009-01-12 CN CN2009801020461A patent/CN101918121B/zh not_active Expired - Fee Related
  • 2009-01-12 DK DK09701040.9T patent/DK2227315T3/en active
  • 2009-01-12 EP EP09701040.9A patent/EP2227315B1/en not_active Not-in-force
• 2011
  • 2011-03-03 HK HK11102175.0A patent/HK1147969A1/zh not_active IP Right Cessation

Patent Citations (2)

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events